KR20230133988A - Livestock wastewater treatment system using molecular decomposition method - Google Patents

Livestock wastewater treatment system using molecular decomposition method Download PDF

Info

Publication number
KR20230133988A
KR20230133988A KR1020220029768A KR20220029768A KR20230133988A KR 20230133988 A KR20230133988 A KR 20230133988A KR 1020220029768 A KR1020220029768 A KR 1020220029768A KR 20220029768 A KR20220029768 A KR 20220029768A KR 20230133988 A KR20230133988 A KR 20230133988A
Authority
KR
South Korea
Prior art keywords
tank
livestock wastewater
contaminants
storage part
activated carbon
Prior art date
Application number
KR1020220029768A
Other languages
Korean (ko)
Inventor
이영선
Original Assignee
이영선
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 이영선 filed Critical 이영선
Priority to KR1020220029768A priority Critical patent/KR20230133988A/en
Publication of KR20230133988A publication Critical patent/KR20230133988A/en

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00—Multistage treatment of water, waste water or sewage
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/28—Mechanical auxiliary equipment for acceleration of sedimentation, e.g. by vibrators or the like
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
    • B01D24/02—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof with the filter bed stationary during the filtration
    • B01D24/10—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof with the filter bed stationary during the filtration the filtering material being held in a closed container
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D39/00—Filtering material for liquid or gaseous fluids
    • B01D39/14—Other self-supporting filtering material ; Other filtering material
    • B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
    • B01D39/2055—Carbonaceous material
    • B01D39/2058—Carbonaceous material the material being particulate
    • B01D39/2062—Bonded, e.g. activated carbon blocks
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D39/00—Filtering material for liquid or gaseous fluids
    • B01D39/14—Other self-supporting filtering material ; Other filtering material
    • B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
    • B01D39/2068—Other inorganic materials, e.g. ceramics
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/02—Treatment of water, waste water, or sewage by heating
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/24—Treatment of water, waste water, or sewage by flotation
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/30—Treatment of water, waste water, or sewage by irradiation
    • C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
    • C02F1/325—Irradiation devices or lamp constructions
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/34—Treatment of water, waste water, or sewage with mechanical oscillations
    • C02F1/36—Treatment of water, waste water, or sewage with mechanical oscillations ultrasonic vibrations
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/48—Treatment of water, waste water, or sewage with magnetic or electric fields
    • C02F1/481—Treatment of water, waste water, or sewage with magnetic or electric fields using permanent magnets
    • C02F1/482—Treatment of water, waste water, or sewage with magnetic or electric fields using permanent magnets located on the outer wall of the treatment device, i.e. not in contact with the liquid to be treated, e.g. detachable
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/48—Treatment of water, waste water, or sewage with magnetic or electric fields
    • C02F1/484—Treatment of water, waste water, or sewage with magnetic or electric fields using electromagnets
    • C02F1/485—Treatment of water, waste water, or sewage with magnetic or electric fields using electromagnets located on the outer wall of the treatment device, i.e. not in contact with the liquid to be treated, e.g. detachable
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/72—Treatment of water, waste water, or sewage by oxidation
    • C02F1/727—Treatment of water, waste water, or sewage by oxidation using pure oxygen or oxygen rich gas
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/72—Treatment of water, waste water, or sewage by oxidation
    • C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/20—Nature of the water, waste water, sewage or sludge to be treated from animal husbandry

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Electromagnetism (AREA)
  • Analytical Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Geology (AREA)
  • Materials Engineering (AREA)
  • Ceramic Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Physical Water Treatments (AREA)

Abstract

본 발명은 분자 분해방식을 이용한 축산폐수의 처리시스템에 관한 것으로,
저류조에 모아진 축산폐수가 비중분리조에서 오염물질들을 분리하면서 부상분리조로 이동하여 부유물을 처리하고, 다음에 분해조와 침전조를 경유하는 중에 오염물들을 분해시키고 분리된 오염물을 부유시키거나 침전시키면서 제거하도록 한 후, 여과조와 치환조를 경유하는 중에 미세한 오염물도 제거하도록 하여 기존의 생물학적 처리방법이 아닌 물리적인 에너지에 의해 오염물을 완전히 분해한 후 분해된 오염물을 원래의 안정한 물질로 전환시켜 자정능력이 뛰어난 양수로 전환하도록 한 것이다.The present invention relates to a treatment system for livestock wastewater using molecular decomposition method.
The livestock wastewater collected in the retention tank separates the contaminants in the gravity separation tank and moves to the flotation separation tank to treat the suspended solids. Then, while passing through the digestion tank and sedimentation tank, the pollutants are decomposed and the separated pollutants are removed by floating or settling. Afterwards, even fine contaminants are removed while passing through the filtration tank and displacement tank, and the contaminants are completely decomposed using physical energy rather than the existing biological treatment method, and the decomposed contaminants are converted into the original stable material to produce pumped water with excellent self-purifying ability. It was to be converted to .

Description

분자 분해방식을 이용한 축산폐수의 처리시스템{omitted}Livestock wastewater treatment system using molecular decomposition method {omitted}

본 발명은 분자 분해방식을 이용한 축산폐수의 처리시스템에 관한 것으로, The present invention relates to a treatment system for livestock wastewater using molecular decomposition method.

특히 저류조에 모아진 축산폐수가 비중분리조에서 오염물질들을 분리하면서 부상분리조로 이동하여 부유물을 처리하고, 다음에 분해조와 침전조를 경유하는 중에 오염물들을 분해시키고 분리된 오염물을 부유시키거나 침전시키면서 제거하도록 한 후, 여과조와 치환조를 경유하는 중에 미세한 오염물도 제거하도록 하여 기존의 생물학적 처리방법이 아닌 물리적인 에너지에 의해 오염물을 완전히 분해한 후 분해된 오염물을 원래의 안정한 물질로 전환시켜 자정능력이 뛰어난 양수로 전환하도록 한 분자 분해방식을 이용한 축산폐수의 처리시스템에 관한 것이다.In particular, the livestock wastewater collected in the retention tank separates contaminants in the gravity separation tank and moves to the flotation separation tank to process the suspended solids. Then, while passing through the decomposer and sedimentation tank, the contaminants are decomposed and the separated contaminants are removed by floating or settling. After that, even fine contaminants are removed while passing through the filtration tank and displacement tank. The contaminants are completely decomposed using physical energy rather than the existing biological treatment method, and the decomposed contaminants are converted to the original stable material, which has excellent self-cleaning ability. This relates to a treatment system for livestock wastewater using a molecular decomposition method that converts it into amniotic fluid.

현대에는 일반 가정이나 공장, 농장 등지에서 쓰레기를 비롯한 걱종 폐기물들이 많이 방출되는 상태이므로 자정(自淨) 능력이 있는 물도 심하게 오염되어 직접 식수로 이용할 수 없음은 물론, 강이나 바다 등의 생태계를 많이 파손하는 실정임은 이미 주지된 사실이다In modern times, as a lot of trash and other types of waste are released from homes, factories, farms, etc., water that has the ability to self-purify is so polluted that it cannot be directly used as drinking water, and ecosystems such as rivers and oceans are greatly damaged. It is already a well-known fact that

그리고 일단 오염된 물은 깨끗하게 하기 위한 정수의 공정으로 여러 가지 장치와 방법을 많이 이용하고 있으며, 지금도 더 효율적인 정수를 위한 연구가 꾸준하게 수행되고 있다.In addition, various devices and methods are used in the water purification process to clean contaminated water, and research on more efficient water purification is still being conducted.

지금까지 알려진 정수의 몇가지 방법을 살펴보면, 활성오니나 미생물울 이용하는 생물학적 방식과, 화학반응을 이용하는 화학적 방식 또는 전자나 초음파를 이용하는 물리적인 방식을 일부 사용하거나 이에 대한 연구를 수행하고 있는 실정이다,Looking at the several methods of water purification known so far, some are being used or research is being conducted on biological methods using activated sludge or microorganisms, chemical methods using chemical reactions, or physical methods using electrons or ultrasound.

그러나 상기와 같은 종래의 오폐수의 정수방식에 의하여서는 안정되고 완전한 정수가 이루어지지 않을 뿐 아니라 정수에 소요되는 가동비가 많아 정수효율을 높일 수 없었다.However, the conventional method of purifying wastewater as described above not only does not achieve stable and complete purification, but also requires a lot of operating costs for purification, making it impossible to increase purification efficiency.

즉, 종래의 활성오니나 미생물을 이용한 생물학적 방식은 미생물이 오염물질을 분해하도록 하는 방식으로 국제적으로 많은 나라에서 이용하고 있으나, 이는 미생물의 소화성 물질에 유효농도라는 한계성이 있으므로 오물이 고농도로 함유된 상태에서는 그 처리가 미흡하고, 알카리나 산성을 띠고 있는 오폐수의 경우는 전처리가 필요하며, 시간과 온도 등의 환경의 영향을 많이 받게 됨은 물론 설치면적이 넓어야 하므로 건설비가 많이 소요되는 등의 단점이 있었다.In other words, the conventional biological method using activated sludge or microorganisms is used in many countries internationally to allow microorganisms to decompose pollutants. However, this method has limitations in the effective concentration of the digestible substances of microorganisms, so it is necessary to use a biological method using activated sludge or microorganisms to allow microorganisms to decompose pollutants. The treatment is insufficient in normal conditions, and in the case of alkaline or acidic wastewater, pretreatment is required, and it is greatly affected by environmental factors such as time and temperature. In addition, the installation area must be large, so construction costs are high. there was.

그리고 화학적 처리방식은 반응속도가 빠르고 공정이 간단하다는 장점이 있는 반면에, 생물학적 처리로 어려운 유기물을 분해시키는 경우라 하더라도 단독으로 폐수를 처리하기 에는 설치비와 유지비가 너무 고가여서 전술한 생물학적 정수방식의 전처리나 후처리로만 사용되는 단점이 있었다.And while the chemical treatment method has the advantage of a fast reaction rate and a simple process, even in the case of decomposing organic substances that are difficult to treat with biological treatment, the installation and maintenance costs are too expensive to treat wastewater alone, so the above-mentioned biological water purification method is difficult to use. It had the disadvantage of being used only as pre- or post-processing.

또한 전자나 초음파를 이용하는 물리적인 방식은 생물학적 방식이나 화학적방식으로 처리가 곤란한 벤젠 화합물이나 할로겐 화합물 등 난분해성 물질을 분해하는 공정에 응용되지만 막대한 시설비와 유지비에 비해 그 효과가 미비한 수준이므로 널리 이용되지 못하는 단점이 있었다.In addition, physical methods using electrons or ultrasonic waves are applied to the process of decomposing non-decomposable substances such as benzene compounds or halogen compounds that are difficult to treat with biological or chemical methods, but are not widely used because their effectiveness is minimal compared to the enormous facility and maintenance costs. There was a downside to not being able to do it.

이에 따라 본 발명은 저류조에 모아진 축산폐수가 비중분리조에서 오염물질들을 분리하면서 부상분리조로 이동하여 부유물을 처리하고, 다음에 분해조와 침전조를 경유하는 중에 오염물들을 분해시키고 분리된 오염물을 부유시키거나 침전시키면서 제거하도록 한 후, 여과조와 치환조를 경유하는 중에 미세한 오염물도 제거하도록 하여 기존의 생물학적 처리방법이 아닌 물리적인 에너지에 의해 오염물을 완전히 분해한 후 분해된 오염물을 원래의 안정한 물질로 전환시켜 자정능력이 뛰어난 양수로 전환하도록 한 분자 분해방식을 이용한 축산폐수의 처리시스템을 제공하는 것을 그 목적으로 한다.Accordingly, in the present invention, the livestock wastewater collected in the storage tank separates the contaminants in the gravity separation tank and moves to the flotation separation tank to treat the suspended solids. Then, while passing through the digestion tank and sedimentation tank, the pollutants are decomposed and the separated pollutants are suspended. After removing it by settling, even fine contaminants are removed while passing through the filtration tank and displacement tank. The contaminants are completely decomposed using physical energy rather than the existing biological treatment method, and then the decomposed contaminants are converted to the original stable material. The purpose is to provide a treatment system for livestock wastewater using a molecular decomposition method that converts it into amniotic fluid with excellent self-purifying ability.

또한 본 발명은 비중분리조에서 오염물질을 원심분리의 방식으로 분리하도록 함은 다른 목적으로 한다.In addition, the present invention has another purpose of separating contaminants in a gravity separation tank by centrifugation.

또한 본 발명은 분해조에서 외벽 둘레의 대향되는 위치에 다수 개의 쌍으로 전자석을 배열하면서 내부에는 전자석에 의해 당겨지는 극성이 접하도록 한 영구자석을 다수의 탄성편에 부착하여 전자석에 의해 당겨지거나 원상태로 환원되는 상태에 의해 진동이 발생하도록 한 상태에서 아래쪽에서는 음이온을, 위쪽에서는 산소를 각각 공급하도록 하여 간단한 구조와 적은 운전비용에도 최대의 분해 효율을 갖도록 함은 다른 목적으로 한다.In addition, the present invention arranges a plurality of pairs of electromagnets in opposing positions around the outer wall in the digester, and attaches a permanent magnet inside which the polarity pulled by the electromagnet is in contact with a plurality of elastic pieces, so that the magnet is pulled by the electromagnet or is in its original state. Another purpose is to ensure maximum decomposition efficiency with a simple structure and low operating cost by supplying negative ions from the bottom and oxygen from the top while causing vibration by the reduction state.

또한 본 발명은 여과조의 여재 및 치환조의 치환재를 다수의 대형 서랍식으로 형성하여 각각의 여재 또는 차환재를 교체할 때 개별 서랍을 교체하는 방식으로 용이하게 처리할 수 있도록 함을 또 다른 목적으로 한다.Another purpose of the present invention is to form the filter medium of the filtration tank and the replacement material of the displacement tank into a plurality of large drawers so that they can be easily handled by replacing individual drawers when replacing each filter medium or replacement material. .

이와 같은 목적을 달성하기 위한 본 발명은 저류조에 모아진 축산폐수가 비중분리조를 경유하는 중에 방전부와 회전유도관과 비중분리대와 침전공간과 청정수 넘침홈 및 청정수 침전실에 의해 원심력으로 오염물질들을 분리되도록 하고,The present invention to achieve this purpose is to remove contaminants by centrifugal force through the discharge section, rotation induction pipe, gravity separator, settling space, clean water overflow groove, and clean water settling chamber while the livestock wastewater collected in the storage tank passes through the gravity separation tank. let them separate,

오염물질이 분리된 축산폐수는 부상분리조로 이동하여 정화를 위해 부유물을 처리하도록 하고,Livestock wastewater from which contaminants have been separated is moved to a flotation separation tank and the suspended matter is treated for purification.

다음에 분해조와 침전조를 경유하는 중에 오염물들을 분해시키고 분리된 오염물을 부유시키거나 침전시키면서 제거하도록 하고,Next, while passing through the digestion tank and sedimentation tank, the contaminants are decomposed and the separated contaminants are removed by floating or settling.

상기의 분해조는 외벽 둘레의 대향되는 위치에 다수 개의 쌍으로 전자석을 배열하면서 내부에는 전자석에 의해 당겨지는 극성이 접하도록 한 영구자석을 다수의 탄성편에 부착하여 전자석에 의해 당겨지거나 원상태로 환원되는 상태에 의해 진동이 발생하도록 한 상태에서 아래쪽에서는 음이온을, 위쪽에서는 산소를 각각 공급하도록 하여 간단한 구조와 적은 운전비용에도 큰 분해 효율을 갖도록 하고,The above-described digester has a plurality of pairs of electromagnets arranged in opposing positions around the outer wall, and inside, permanent magnets with the polarity pulled by the electromagnets in contact are attached to a plurality of elastic pieces, so that they can be pulled by the electromagnets or restored to their original state. With vibration occurring depending on the condition, negative ions are supplied from the bottom and oxygen are supplied from the top, enabling high decomposition efficiency despite a simple structure and low operating cost.

여과조와 치환조를 경유하는 중에 미세한 오염물도 제거하도록 하여 기존의 생물학적 처리방법이 아닌 물리적인 에너지에 의해 오염물을 완전히 분해한 후 분해된 오염물을 원래의 안정한 물질로 전환시켜 자정능력이 뛰어난 양수로 전환하도록 하고,By removing even the finest contaminants while passing through the filtration tank and displacement tank, the contaminants are completely decomposed using physical energy rather than existing biological treatment methods, and then the decomposed contaminants are converted to the original stable substances, converting them into pumped water with excellent self-purifying ability. Let's do it,

상기 여과조의 여재 및 치환조의 치환재를 다수의 대형 서랍식으로 형성하여 각각의 여재 또는 차환재를 교체할 때 개별 서랍을 교체하는 방식으로 용이하게 처리할 수 있도록 하여 미세한 오염물도 제거하도록 하고,The filter medium of the filtration tank and the replacement material of the displacement tank are formed in a plurality of large drawers so that they can be easily processed by replacing individual drawers when replacing each filter medium or replacement material, so that even fine contaminants can be removed,

산소공급조에서 용존산소량을 높여주도록 하여 기존의 생물학적 처리 방법이 아닌 물리적인 에너지에 의해 오염물을 완전히 분해한 후 분해된 오염물을 원래의 안정한 물질로 전환시켜 자정능력이 뛰어난 양수로 전환하도록 한 것이다.By increasing the amount of dissolved oxygen in the oxygen supply tank, the contaminants are completely decomposed using physical energy rather than the existing biological treatment method, and then the decomposed contaminants are converted to the original stable substances and converted into amniotic fluid with excellent self-purifying ability.

본 발명의 분자 분해방식을 이용한 축산폐수의 처리시스템에 의하여서는 저류조에 모아진 축산폐수가 비중분리조를 경유하는 중에 정화를 위해 회전에 의한 원심력으로 오염물질들이 분리되도록 한 후 부상분리조로 이동하여 정화를 위해 부유물을 처리하도록 하고,According to the livestock wastewater treatment system using the molecular decomposition method of the present invention, while the livestock wastewater collected in the retention tank passes through the gravity separation tank, contaminants are separated by centrifugal force due to rotation for purification, and then moved to the flotation separation tank for purification. to dispose of floating matter for

다음에 분해조와 침전조를 차례로 경유하는 중에 축산폐수에 포함된 오염물들을 분해시킨 상태에서 분리된 오염물을 부유시키거나 침전시키면서 제거하도록 하고,Next, while passing through the decomposition tank and the sedimentation tank sequentially, the contaminants contained in the livestock wastewater are decomposed and removed by suspending or settling the separated contaminants.

상기의 분해조는 외벽 둘레의 대향되는 위치에 다수 개의 쌍으로 전자석을 배열하면서 내부에는 전자석에 의해 당겨지는 극성이 접하도록 한 영구자석을 다수의 탄성편에 부착하여 전자석에 의해 당겨지거나 원상태로 환원되는 상태에 의해 진동이 발생하도록 한 상태에서 아래쪽에서는 음이온을, 위쪽에서는 산소를 각각 공급하도록 하여 간단한 구조와 적은 운전비용에도 큰 분해 효율을 갖도록 하고,The above-described digester has a plurality of pairs of electromagnets arranged in opposing positions around the outer wall, and inside, permanent magnets with the polarity pulled by the electromagnets in contact are attached to a plurality of elastic pieces, so that they can be pulled by the electromagnets or restored to their original state. With vibration occurring depending on the condition, negative ions are supplied from the bottom and oxygen are supplied from the top, enabling high decomposition efficiency despite a simple structure and low operating cost.

다수의 대형 서랍식으로 형성하여 여재 및 치환재를 교체할 때 개별 서랍을 교체하는 방식으로 용이하게 관리할 있도록 한 여과조 및 치환조를 통해 미세한 오염물도 제거하도록 하는 효과가 있다.It has the effect of removing even fine contaminants through the filtration tank and displacement tank, which are formed in a plurality of large drawers and can be easily managed by replacing individual drawers when replacing the filter medium and displacement material.

도 1은 본 발명의 전체적인 구성을 개략적으로 나타낸 계통도.
도 2는 본 발명 비중분리조의 구성을 도시한 개략도.
도 3은 본 발명 부상분리조의 구성을 도시한 개략도.
도 4는 본 발명의 분해조의 구성을 도시한 개략도.
도 5는 본 발명의 침전조의 구성을 도시한 개략도.
도 6은 본 발명 여과조의 구성을 도시한 개략도.
도 7은 본 발명 치환조의 구성을 도시한 개략도.1 is a schematic diagram schematically showing the overall configuration of the present invention.
Figure 2 is a schematic diagram showing the configuration of the gravity separation tank of the present invention.
Figure 3 is a schematic diagram showing the configuration of the flotation separation tank of the present invention.
Figure 4 is a schematic diagram showing the configuration of the digestion tank of the present invention.
Figure 5 is a schematic diagram showing the configuration of a sedimentation tank of the present invention.
Figure 6 is a schematic diagram showing the configuration of the filtration tank of the present invention.
Figure 7 is a schematic diagram showing the configuration of the substitution tank of the present invention.

도 1 내지 도 7은 본 발명 의 구성을 도시한 것으로서,1 to 7 show the configuration of the present invention,

저류조에 모아진 축산폐수가 오염수입구(1a)를 통해 유입되어 방전부(2)과 회전유도관(3)의 영향으로 회전하도록 하면서 비중분리대(4)의 비중분리날개(4a)와 부딪쳐 침전물이 하부 안정공간(5)에 침전되어 슬러지 배출구(1b)로 배출하도록 하고 슬러지가 분리된 축산폐수는 침전실(7)의 넘침홈(6)을 통해 잔여 슬러지를 침전시킨 후 축산폐수만 청정수 출구(1c)로 토출하도록 한 비중분리조(1)와,The livestock wastewater collected in the storage tank flows in through the contaminated inlet (1a) and rotates under the influence of the discharge part (2) and the rotation guide pipe (3), and hits the gravity separation wing (4a) of the gravity separator (4), causing sediment to form. It settles in the lower stable space (5) and is discharged through the sludge discharge port (1b). The livestock wastewater from which the sludge is separated is allowed to settle the remaining sludge through the overflow groove (6) of the settling chamber (7), and then only the livestock wastewater is discharged through the clean water outlet ( A specific gravity separation tank (1) designed to discharge to 1c),

상기 비중분리조(1)로부터 슬러지가 제거된 축산폐수를 공급받으면서 일측 내벽의 초음파 발생기(11), 영구자석(13)이 부착된 자화판(12), 펌프(15)를 통해 폭기조(16)로 음이온을 공급하는 음이온 산소발생기(14)에 의해 부유물을 내부의 부상공간(17)으로 부상시키도록 한 부상분리조(10)와,While receiving livestock wastewater from which sludge has been removed from the gravity separation tank (1), the aeration tank (16) is supplied through an ultrasonic generator (11) on one inner wall, a magnetized plate (12) with a permanent magnet (13) attached thereto, and a pump (15). a flotation separator (10) in which suspended matter is made to float to the internal flotation space (17) by an anion oxygen generator (14) that supplies negative ions;

상기의 부유물이 분리된 분리된 축산폐수를 공급받으며 외벽이나 내벽 둘레의 대향되는 위치에 다수 개의 쌍으로 전자석(21)을 배열하면서 내부에는 전자석(21)에 의해 당겨지는 극성이 접하도록 한 영구자석(22)을 다수의 탄성편(23)에 부착하여 전자석(21)에 의해 당겨지거나 원상태로 환원되는 상태에 의해 진동이 발생하도록 하고 아래쪽에서는 음이온발생기(24)를 통한 공기와 오존발생기(26)를 통한 공기를 각각 음이온공급구(25)와 오존공급구(27)를 통하여 공급하도록 하며 상부에는 산소공급기(28)로부터 산소를 산소공급구(29)를 통하여 공급하도록 하고 내부에는 각각 투명관에 내장한 다수의 UV램프(30)와 다수의 히터(31)를 설치하여 축산폐수를 분해하는 분해조(20)와,A permanent magnet is supplied with separated livestock wastewater from which the floating matter is separated, and electromagnets (21) are arranged in multiple pairs at opposing positions around the outer or inner wall, and the polarity pulled by the electromagnets (21) are in contact with each other inside. (22) is attached to a plurality of elastic pieces (23) to generate vibration by being pulled by the electromagnet (21) or returned to its original state, and at the bottom, air and ozone generator (26) are generated through the negative ion generator (24). Air is supplied through the negative ion supply port (25) and ozone supply port (27), and oxygen is supplied from the oxygen supply port (28) at the top through the oxygen supply port (29), and inside each transparent tube. A digestion tank (20) that decomposes livestock wastewater by installing a plurality of built-in UV lamps (30) and a plurality of heaters (31),

상기의 분해조(20)에서 축산폐수와 오염물을 공급받아 경사 바닥면(41)에 가라앉은 슬러지를 모터(42)에 연결된 축(43)을 중심으로 스트레나(44)로 제거하는 침전조(40)와,A settling tank (40) that receives livestock wastewater and contaminants from the digestion tank (20) and removes the sludge settled on the inclined bottom surface (41) with a strainer (44) centered on a shaft (43) connected to the motor (42). and,

상기의 침전조(40)로부터 축산폐수를 공급받아 내부의 여재(51)로 오염물을 여과하는 여과조(50)와,A filtration tank (50) that receives livestock wastewater from the settling tank (40) and filters contaminants through an internal filter medium (51);

상기 여과조(50)로부터 축산폐수를 공급받아 내부의 치환재(61) 및 교변 전자석(62)에 의해 자화시키면서 활성화하는 치환조(60)들로 구성한 것이다.It is composed of a displacement tank (60) that receives livestock wastewater from the filtration tank (50) and activates it by magnetizing it with an internal displacement material (61) and a shifting electromagnet (62).

그리고 상기의 여과조(50)는,And the above-mentioned filtration tank 50,

상기의 침전조(40)로부터 축산폐수를 공급받아 내부의 여재(51)를 통해 오염물을 여과하도록 하되,Livestock wastewater is supplied from the above sedimentation tank (40) and contaminants are filtered through the internal filter media (51).

제올라이트 수납부(52)와 칠보석 수납부(53)와 폐석탄 수납부(54)와 활성탄 수납부(55) 그리고 여유 수납부(56)를 서랍식으로 형성하여 각각의 공간에 5~10cm의 크기로 파쇄한 제올라이트와 칠보석과 폐석탄 및 활성탄을 각각 충진하면서 여재(51)를 이루도록 함으로써 여유 수납부(56)에 새로운 제올라이트와 칠보석과 폐석탄 및 활성탄을 채우면서 각 수납부(52)(53)(54)(55)의 청소는 물론 여재의 교환이 용이하도록 한 것이다.The zeolite storage section (52), the lacquer storage section (53), the waste coal storage section (54), the activated carbon storage section (55), and the spare storage section (56) are formed in a drawer style, each space having a size of 5 to 10 cm. By filling the crushed zeolite, lacquer, waste coal, and activated carbon to form the filter medium 51, the spare storage portion 56 is filled with new zeolite, lacquer, waste coal, and activated carbon, filling each storage portion 52 ( This makes it easy to clean 53)(54)(55) as well as replace the filter media.

상기의 치환조(60)는,The above substitution tank (60),

상기 여과조(50)로부터 축산폐수를 공급받아 내부의 치환재(61) 및 교변 전자석(62)에 의해 자화시키면서 활성화하도록 하되,Livestock wastewater is supplied from the filtration tank (50) and activated by magnetization by the internal displacement material (61) and the alternating electromagnet (62),

게르마늄 수납부(63)와 폐석탄 수납부(64)와 활성탄 수납부(65)와 포졸란 수납부(66)와 칠보석 수납부(67) 그리고 여유 수납부(68)로 구성하여 5~10cm의 크기로 파쇄한 게르마늄과 폐석탄과 활성탄과 포졸란 및 칠보석을 각각 충진하여 치환재(61)를 이루도록 함으로써 여유 수납부(56)에 새로운 게르마늄과 폐석탄과 활성탄과 포졸란 및 칠보석을 채우면서 각 수납부(63)(64)(65)(66)(67)의 청소는 물론 치환재의 교환이 용이하도록 한 것이다.It is composed of a germanium storage part (63), a waste coal storage part (64), an activated carbon storage part (65), a pozzolan storage part (66), a lacquered jewel storage part (67), and a spare storage part (68), and a 5 to 10 cm spacer. By filling the crushed germanium, waste coal, activated carbon, pozzolan, and lacquered stones respectively to form the replacement material 61, the spare storage part 56 is filled with new germanium, waste coal, activated carbon, pozzolan, and lacquered stones. This is to facilitate cleaning of the storage portions 63, 64, 65, 66, and 67 as well as replacement of replacement materials.

상기의 분해조(20)와 침전조(40)와 여과조(50) 및 치환조(60)는 축산폐수의 상태에 따라 2회 이상 설치하여 축산폐수의 분해와 침전과 여과 및 치환의 과정이 2회 이상 반복적으로 행해지도록 구성한 것이다.The decomposition tank 20, sedimentation tank 40, filtration tank 50, and displacement tank 60 are installed two or more times depending on the condition of the livestock wastewater, so that the processes of decomposition, sedimentation, filtration, and substitution of the livestock wastewater are carried out twice. It is designed to be performed repeatedly.

이와 같이 구성한 본 발명의 분자 분해방식을 이용한 축산폐수의 처리시스템은 저류조에 모아진 축산폐수가 비중분리조(1)의 오염수입구(1a)를 통해 유입되어 방전부(2)과 회전유도관(3)의 영향으로 회전하도록 하면서 비중분리대(4)의 비중분리날개(4a)와 부딪쳐 침전물이 하부 안정공간(5)에 침전되도록 한다.In the livestock wastewater treatment system using the molecular decomposition method of the present invention constructed in this way, the livestock wastewater collected in the storage tank flows into the contaminated inlet (1a) of the gravity separation tank (1), and flows into the discharge unit (2) and the rotation induction pipe ( While rotating under the influence of 3), it collides with the gravity separation wing (4a) of the gravity separator (4), causing the sediment to settle in the lower stable space (5).

그 과정에서 상대적으로 무거운 슬러지는 슬러지 배출구(1b)로 배출하도록 하면서 슬러지가 분리된 축산폐수는 침전실(7)의 넘침홈(6)을 통해 잔여 슬러지를 침전시킨 후 축산폐수만 청정수 출구(1c)로 토출하도록 한다.In the process, the relatively heavy sludge is discharged to the sludge discharge port (1b), and the livestock wastewater from which the sludge is separated is allowed to settle the remaining sludge through the overflow groove (6) of the settling chamber (7), and then only the livestock wastewater is discharged to the clean water outlet (1c). ) to discharge it.

상기 비중분리조(1)로부터 슬러지가 제거된 축산폐수를 공급받는 부상분리조(10)에서 일측 내벽의 초음파 발생기(11)로부터의 초음파, 자화판(12)에 부착된 영구자석(13)으로부터의 자기장에너지, 음이온 산소발생기(14)에서 펌프(15)를 통해 폭기조(16)로 공급되는 음이온에 의해 부유물을 내부의 부상공간(17)으로 부상시키도록 한다.In the flotation separation tank (10), which receives livestock wastewater from which sludge has been removed from the gravity separation tank (1), ultrasonic waves come from the ultrasonic generator (11) on one inner wall, and from the permanent magnet (13) attached to the magnetized plate (12). The magnetic field energy and negative ions supplied from the negative ion oxygen generator 14 to the aeration tank 16 through the pump 15 cause suspended matter to float to the internal flotation space 17.

상기의 부유물이 분리된 축산폐수를 공급받는 분해조(20)에서는 외벽이나 내벽 둘레의 대향되는 위치에 다수 개의 쌍으로 전자석(21)을 배열하면서 내부에는 전자석(21)에 의해 당겨지는 극성이 접하도록 한 영구자석(22)을 다수의 탄성편(23)에 부착하여 전자석(21)에 의해 당겨지거나 원상태로 환원되는 상태에 의해 발생하는 진동에 의해 내부의 축산폐수의 분해가 이루어지도록 한다.In the digester 20, which receives the livestock wastewater from which the suspended matter has been separated, a plurality of pairs of electromagnets 21 are arranged at opposing positions around the outer or inner wall, and the polarity pulled by the electromagnets 21 is folded inside. A permanent magnet (22) is attached to a plurality of elastic pieces (23) so that the internal livestock wastewater is decomposed by vibration generated by being pulled by the electromagnet (21) or being returned to its original state.

그리고 아래쪽에서는 음이온발생기(24)를 통한 공기와 오존발생기(26)를 통한 공기를 각각 음이온공급구(25)와 오존공급구(27)를 통하여 공급하도록 하는 동시에 상부에는 산소공급기(28)로부터 산소를 산소공급구(29)를 통하여 공급하도록 함으로써 축산폐수의 비중에 따른 분해가 원활하게 이루어지도록 한다.And at the bottom, air through the negative ion generator 24 and air through the ozone generator 26 are supplied through the negative ion supply port 25 and the ozone supply port 27, respectively, while at the top, oxygen is supplied from the oxygen supply device 28. By supplying it through the oxygen supply port (29), decomposition according to the specific gravity of the livestock wastewater is carried out smoothly.

또한 내부에 각각 투명관에 내장하면서 설치한 다수의 UV램프(30)와 다수의 히터(31)에 의한 자외선과 열 및 빛에너지에 의해 축산폐수의 분해가 더 원활하게 이루어지도록 한다.In addition, the decomposition of livestock wastewater is carried out more smoothly by ultraviolet rays, heat, and light energy generated by a plurality of UV lamps (30) and a plurality of heaters (31) installed inside each transparent tube.

상기의 분해조(20)에서 축산폐수와 오염물을 공급받는 침전조(40)에서는 경사 바닥면(41)에 가라앉은 슬러지를 모터(42)에 연결된 축(43)을 중심으로 스트레나(44)로 제거하도록 한다.In the settling tank 40, which receives livestock wastewater and contaminants from the digestion tank 20, the sludge settled on the inclined bottom surface 41 is removed with a strainer 44 centered on a shaft 43 connected to the motor 42. Let's do it.

상기의 침전조(40)로부터 축산폐수를 공급받는 여과조(50)에서는 내부의 여재(51)로 오염물을 여과하도록 한다.In the filtration tank 50, which receives livestock wastewater from the settling tank 40, contaminants are filtered through an internal filter medium 51.

즉 상기의 여과조(50)는 제올라이트 수납부(52)와 칠보석 수납부(53)와 폐석탄 수납부(54)와 활성탄 수납부(55) 그리고 여유 수납부(56)를 서랍식으로 형성하여 각각의 공간에 5~10cm의 크기로 파쇄한 제올라이트와 칠보석과 폐석탄 및 활성탄을 각각 충진하면서 여재(51)를 이루도록 함으로써 여유 수납부(56)에 새로운 제올라이트와 칠보석과 폐석탄 및 활성탄을 채우면서 각 수납부(52)(53)(54)(55)의 청소는 물론 여재의 교환이 용이하도록 한다.That is, the filtration tank 50 is formed with a zeolite storage section 52, a lacquer storage section 53, a waste coal storage section 54, an activated carbon storage section 55, and a spare storage section 56 in a drawer type, respectively. By filling the space with shredded zeolite, lacquerware, waste coal, and activated carbon to a size of 5 to 10 cm, respectively, to form a filter medium (51), the spare storage portion (56) is filled with new zeolite, lacquerware, waste coal, and activated carbon. This makes it easy to clean each storage part (52, 53, 54, and 55) as well as replace the filter medium.

상기 여과조(50)로부터 축산폐수를 공급받는 치환조(60)에서는 내부의 치환재(61) 및 교변 전자석(62)에 의해 자화시키면서 활성화하도록 한다.In the displacement tank 60, which receives livestock wastewater from the filtration tank 50, it is magnetized and activated by the internal displacement material 61 and the alternating electromagnet 62.

즉 상기의 치환조(60)는,That is, the substitution tank 60 described above is,

게르마늄 수납부(63)와 폐석탄 수납부(64)와 활성탄 수납부(65)와 포졸란 수납부(66)와 칠보석 수납부(67) 그리고 여유 수납부(68)로 구성하여 5~10cm의 크기로 파쇄한 게르마늄과 폐석탄과 활성탄과 포졸란 및 칠보석을 각각 충진하여 치환재(61)를 이루도록 함으로써 여유 수납부(56)에 새로운 게르마늄과 폐석탄과 활성탄과 포졸란 및 칠보석을 채우면서 각 수납부(63)(64)(65)(66)(67)의 청소는 물론 치환재의 교환이 용이하도록 한다.It is composed of a germanium storage part (63), a waste coal storage part (64), an activated carbon storage part (65), a pozzolan storage part (66), a lacquered jewel storage part (67), and a spare storage part (68), and a 5 to 10 cm spacer. By filling the crushed germanium, waste coal, activated carbon, pozzolan, and lacquered stones respectively to form the replacement material 61, the spare storage part 56 is filled with new germanium, waste coal, activated carbon, pozzolan, and lacquered stones. It makes it easy to clean the storage parts (63) (64) (65) (66) (67) as well as replace the replacement material.

상기의 분해조(20)와 침전조(40)와 여과조(50) 및 치환조(60)는 축산폐수의 상태에 따라 2회 이상 설치하여 축산폐수의 분해와 침전과 여과 및 치환의 과정이 2회 이상 반복적으로 행해지도록 한다.The decomposition tank 20, sedimentation tank 40, filtration tank 50, and displacement tank 60 are installed two or more times depending on the condition of the livestock wastewater, so that the processes of decomposition, sedimentation, filtration, and substitution of the livestock wastewater are carried out twice. It should be done repeatedly.

그리고 상기 여과조(50)의 여재(51) 그리고 치환조(60)의 치환재(61)는 축산폐수에 존재하는 불안정한 분해물을 OH라디칼과 함께 흡수하면서 안정화되도록 하고 스스로 라디칼화가 이루어지도록 한다.In addition, the filter medium 51 of the filtration tank 50 and the displacement medium 61 of the displacement tank 60 stabilize the unstable decomposition products present in livestock wastewater by absorbing them with OH radicals and allow radicalization to occur on their own.

또한 축산폐수는 치환조(60)의 교변전자석(62)에 의해 자화되고 활성화되어 미네랄이 풍부한 게르마늄등을 거치는 동안 물의 구조가 큰물분자로 변화하며 반응성이 높은 전자와 OH라디칼 등은 치환재에 의해 흡수되어 분해수는 안정화 된다.In addition, livestock wastewater is magnetized and activated by the alternating electromagnet 62 of the displacement tank 60, and while passing through germanium, which is rich in minerals, the structure of the water changes into large water molecules, and highly reactive electrons and OH radicals are removed by the displacement agent. By absorption, the decomposition water is stabilized.

이러한 경로를 거쳐 축산폐수는 자정능력이 아주 뛰어난 물로 전환되어 물속에 존재하는 미세한 오염물도 제거되므로 방류하면 된다Through this route, livestock wastewater is converted into water with excellent self-purifying ability, and even fine contaminants present in the water are removed, so it can be discharged.

1 : 비중분리조 10 : 부상분리조
20 : 분해조 40 : 침전조
50 : 여과조 60 : 치환조1: Specific gravity separation tank 10: Flotation separation tank
20: digestion tank 40: sedimentation tank
50: filtration tank 60: displacement tank

Claims (4)

저류조에 모아진 축산폐수가 오염수입구(1a)를 통해 유입되어 방전부(2)과 회전유도관(3)의 영향으로 회전하도록 하면서 비중분리대(4)의 비중분리날개(4a)와 부딪쳐 침전물이 하부 안정공간(5)에 침전되어 슬러지 배출구(1b)로 배출하도록 하고 슬러지가 분리된 축산폐수는 침전실(7)의 넘침홈(6)을 통해 잔여 슬러지를 침전시킨 후 축산폐수만 청정수 출구(1c)로 토출하도록 한 비중분리조(1)와,
상기 비중분리조(1)로부터 슬러지가 제거된 축산폐수를 공급받으면서 일측 내벽의 초음파 발생기(11), 영구자석(13)이 부착된 자화판(12), 펌프(15)를 통해 폭기조(16)로 음이온을 공급하는 음이온 산소발생기(14)에 의해 부유물을 내부의 부상공간(17)으로 부상시키도록 한 부상분리조(10)와,
상기의 부유물이 분리된 분리된 축산폐수를 공급받으며 외벽이나 내벽 둘레의 대향되는 위치에 다수 개의 쌍으로 전자석(21)을 배열하면서 내부에는 전자석(21)에 의해 당겨지는 극성이 접하도록 한 영구자석(22)을 다수의 탄성편(23)에 부착하여 전자석(21)에 의해 당겨지거나 원상태로 환원되는 상태에 의해 진동이 발생하도록 하고 아래쪽에서는 음이온발생기(24)를 통한 공기와 오존발생기(26)를 통한 공기를 각각 음이온공급구(25)와 오존공급구(27)를 통하여 공급하도록 하며 상부에는 산소공급기(28)로부터 산소를 산소공급구(29)를 통하여 공급하도록 하고 내부에는 각각 투명관에 내장한 다수의 UV램프(30)와 다수의 히터(31)를 설치하여 축산폐수를 분해하는 분해조(20)와,
상기의 분해조(20)에서 축산폐수와 오염물을 공급받아 경사 바닥면(41)에 가라앉은 슬러지를 모터(42)에 연결된 축(43)을 중심으로 스트레나(44)로 제거하는 침전조(40)와,
상기의 침전조(40)로부터 축산폐수를 공급받아 내부의 여재(51)로 오염물을 여과하는 여과조(50)와,
상기 여과조(50)로부터 축산폐수를 공급받아 내부의 치환재(61) 및 교변 전자석(62)에 의해 자화시키면서 활성화하는 치환조(60)들로 구성한 것을 특징으로 하는 분자 분해방식을 이용한 축산폐수의 처리시스템.The livestock wastewater collected in the storage tank flows in through the contaminated inlet (1a) and rotates under the influence of the discharge part (2) and the rotation guide pipe (3), and hits the gravity separation wing (4a) of the gravity separator (4), causing sediment to form. It settles in the lower stable space (5) and is discharged through the sludge discharge port (1b). The livestock wastewater from which the sludge is separated is allowed to settle the remaining sludge through the overflow groove (6) of the settling chamber (7), and then only the livestock wastewater is discharged through the clean water outlet ( A specific gravity separation tank (1) designed to discharge to 1c),
While receiving livestock wastewater from which sludge has been removed from the gravity separation tank (1), the aeration tank (16) is supplied through an ultrasonic generator (11) on one inner wall, a magnetized plate (12) with a permanent magnet (13) attached thereto, and a pump (15). a flotation separator (10) in which suspended matter is made to float to the internal flotation space (17) by an anion oxygen generator (14) that supplies negative ions;
A permanent magnet is supplied with separated livestock wastewater from which the floating matter is separated, and electromagnets (21) are arranged in multiple pairs at opposing positions around the outer or inner wall, and the polarity pulled by the electromagnets (21) are in contact with each other inside. (22) is attached to a plurality of elastic pieces (23) to generate vibration by being pulled by the electromagnet (21) or returned to its original state, and at the bottom, air and ozone generator (26) are generated through the negative ion generator (24). Air is supplied through the negative ion supply port (25) and ozone supply port (27), and oxygen is supplied from the oxygen supply port (28) at the top through the oxygen supply port (29), and inside each transparent tube. A decomposition tank (20) that decomposes livestock wastewater by installing a number of built-in UV lamps (30) and a number of heaters (31),
A settling tank (40) that receives livestock wastewater and contaminants from the digestion tank (20) and removes the sludge settled on the inclined bottom surface (41) with a strainer (44) centered on a shaft (43) connected to the motor (42). and,
A filtration tank (50) that receives livestock wastewater from the settling tank (40) and filters contaminants through an internal filter medium (51);
Livestock wastewater using a molecular decomposition method, characterized in that it is composed of a displacement tank (60) that receives livestock wastewater from the filtration tank (50) and activates it by magnetizing it by an internal displacement material (61) and a shifting electromagnet (62). Processing system. 청구항 1에 있어서,
상기의 여과조(50)는,
상기의 침전조(40)로부터 축산폐수를 공급받아 내부의 여재(51)를 통해 오염물을 여과하도록 하되,
제올라이트 수납부(52)와 칠보석 수납부(53)와 폐석탄 수납부(54)와 활성탄 수납부(55) 그리고 여유 수납부(56)를 서랍식으로 형성하여 각각의 공간에 5~10cm의 크기로 파쇄한 제올라이트와 칠보석과 폐석탄 및 활성탄을 각각 충진하면서 여재(51)를 이루도록 함으로써 여유 수납부(56)에 새로운 제올라이트와 칠보석과 폐석탄 및 활성탄을 채우면서 각 수납부(52)(53)(54)(55)의 청소는 물론 여재의 교환이 용이하도록 구성한 것을 특징으로 하는 분자 분해방식을 이용한 축산폐수의 처리시스템.In claim 1,
The filtration tank 50 described above is,
Livestock wastewater is supplied from the above sedimentation tank (40) and contaminants are filtered through the internal filter media (51).
The zeolite storage section (52), the lacquer storage section (53), the waste coal storage section (54), the activated carbon storage section (55), and the spare storage section (56) are formed in a drawer style, each space having a size of 5 to 10 cm. By filling the crushed zeolite, lacquer, waste coal, and activated carbon to form the filter medium 51, the spare storage portion 56 is filled with new zeolite, lacquer, waste coal, and activated carbon, filling each storage portion 52 ( 53)(54)(55) A livestock wastewater treatment system using molecular decomposition, characterized in that it is configured to facilitate cleaning of the filter medium as well as exchange of the filter medium. 청구항 1에 있어서,
상기의 치환조(60)는,
상기 여과조(50)로부터 축산폐수를 공급받아 내부의 치환재(61) 및 교변 전자석(62)에 의해 자화시키면서 활성화하도록 하되,
게르마늄 수납부(63)와 폐석탄 수납부(64)와 활성탄 수납부(65)와 포졸란 수납부(66)와 칠보석 수납부(67) 그리고 여유 수납부(68)로 구성하여 5~10cm의 크기로 파쇄한 게르마늄과 폐석탄과 활성탄과 포졸란 및 칠보석을 각각 충진하여 치환재(61)를 이루도록 함으로써 여유 수납부(56)에 새로운 게르마늄과 폐석탄과 활성탄과 포졸란 및 칠보석을 채우면서 각 수납부(63)(64)(65)(66)(67)의 청소는 물론 치환재의 교환이 용이하도록 구성한 것을 특징으로 하는 분자 분해방식을 이용한 축산폐수의 처리시스템.In claim 1,
The above substitution tank (60),
Livestock wastewater is supplied from the filtration tank (50) and activated by magnetization by the internal displacement material (61) and the alternating electromagnet (62),
It is composed of a germanium storage part (63), a waste coal storage part (64), an activated carbon storage part (65), a pozzolan storage part (66), a lacquered jewel storage part (67), and a spare storage part (68), and a 5 to 10 cm spacer. By filling the crushed germanium, waste coal, activated carbon, pozzolan, and lacquered stones respectively to form the replacement material 61, the spare storage part 56 is filled with new germanium, waste coal, activated carbon, pozzolan, and lacquered stones. A livestock wastewater treatment system using a molecular decomposition method, characterized in that it is configured to facilitate cleaning of the storage portion (63) (64) (65) (66) (67) as well as replacement of replacement materials. 청구항 1에 있어서,
상기의 분해조(20)와 침전조(40)와 여과조(50) 및 치환조(60)는 축산폐수의 상태에 따라 2회 이상 설치하여 축산폐수의 분해와 침전과 여과 및 치환의 과정이 2회 이상 반복적으로 행해지도록 구성한 것을 특징으로 하는 분자 분해방식을 이용한 축산폐수의 처리시스템.In claim 1,
The decomposition tank 20, sedimentation tank 40, filtration tank 50, and displacement tank 60 are installed two or more times depending on the condition of the livestock wastewater, so that the processes of decomposition, sedimentation, filtration, and substitution of the livestock wastewater are carried out twice. A treatment system for livestock wastewater using a molecular decomposition method, characterized in that it is configured to be performed repeatedly.
KR1020220029768A 2022-03-10 2022-03-10 Livestock wastewater treatment system using molecular decomposition method KR20230133988A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1020220029768A KR20230133988A (en) 2022-03-10 2022-03-10 Livestock wastewater treatment system using molecular decomposition method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1020220029768A KR20230133988A (en) 2022-03-10 2022-03-10 Livestock wastewater treatment system using molecular decomposition method

Publications (1)

Publication Number Publication Date
KR20230133988A true KR20230133988A (en) 2023-09-20

Family

ID=88192038

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1020220029768A KR20230133988A (en) 2022-03-10 2022-03-10 Livestock wastewater treatment system using molecular decomposition method

Country Status (1)

Country Link
KR (1) KR20230133988A (en)

Similar Documents

Publication Publication Date Title
KR100848117B1 (en) Advanced water treatment equipment
JP2002273261A (en) Membrane magnetic separation device
KR100406190B1 (en) Filter type upflow filter with double treatment tank
CN101638277A (en) Car washing water purification recycling processing system
CN111170394A (en) Emission reduction method and device for volatile organic compounds in oily sewage cleaning treatment
KR20130109631A (en) Water treatment apparatus for purifing waste water using natural energy
KR100882452B1 (en) A waste water disposal plant with advanced ozone contact filter type
KR101233696B1 (en) Apparatus for treating water and apparatus for treating waste water using the same
KR20230133988A (en) Livestock wastewater treatment system using molecular decomposition method
KR100538347B1 (en) Sewage and wastewater treatment apparatus
KR100711259B1 (en) Purification treatment apparatus
CN114212853B (en) Air floatation tank for demulsification of emulsified oil-containing wastewater, wastewater treatment system comprising air floatation tank and method
JP4044292B2 (en) Wastewater treatment equipment
KR20230167258A (en) Water treatment system using back washing filter
KR200384037Y1 (en) Water separation apparatus of waste water disposal system
KR200334439Y1 (en) Apparatus for treatment of waste water or sludge
WO2021255541A1 (en) Plant for purifying wastewater
KR101499777B1 (en) Water Purification System Unified Settling Tank and Aeration Tank
KR101070172B1 (en) purification device
KR200413336Y1 (en) Modified sewage and wastewater treatment apparatus
JP5266436B2 (en) Organic wastewater treatment method and apparatus
KR20010026445A (en) Sewage and waste water treating system using molecular decomposition
CN111151090A (en) Comprehensive treatment method for waste water and waste gas
KR101885134B1 (en) waste water continual system and method
CN219950661U (en) Ozone air floatation device

Legal Events

Date Code Title Description
E902 Notification of reason for refusal
E601 Decision to refuse application